US2007181436A1PendingUtilityA1
Production of Titanium
Est. expiryJun 28, 2024(expired)· nominal 20-yr term from priority
B22F 2998/00C25C 3/28C22B 34/129C25C 5/04C22B 1/2406
39
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Claims
Abstract
A method of producing titanium semi-finished or ready-to-use products from titanium oxide powders and/or pellets is disclosed. The method produces products that are not affected adversely by levels of chlorine that have an impact on performance, particularly weldability, of products made by other methods.
Claims
exact text as granted — not AI-modified1 . A method of producing titanium products comprising:
(a) electrochemically reducing titanium oxide in an electrolytic cell that includes an anode, a cathode, and a molten electrolyte that includes cations of a metal that is capable of chemically reducing titanium oxide and chloride anions; and (b) processing the titanium product of step (a) and forming one of a semi-finished or ready-to-use product having a concentration of chlorine of at least 100 ppm.
2 . The method defined in claim 1 wherein the titanium oxide is in the form of a powder or pellet.
3 . The method defined in claim 2 wherein the titanium oxide powder or pellet has a size of 3.5 mm or less in a minor dimension of the powder or pellet.
4 . The method defined in claim 2 wherein the size of the titanium oxide powder or pellet is less than 2.5 mm in the minor dimension of the powder or pellet.
5 . The method defined in claim 2 wherein the size of the powder or pellet is 1-2 mm in the minor dimension of the powder or pellet.
6 . The method defined in claim 1 wherein step (a) includes electrochemically reducing titanium oxide to titanium metal having a concentration of oxygen that is no more than 0.5% by weight.
7 . The method defined in claim 6 wherein the oxygen concentration is no more than 0.3% by weight.
8 . The method defined in claim 6 wherein the oxygen concentration is no more than 0.1% by weight.
9 . The method defined in claim 1 wherein the electrolyte is a CaCl 2 -based electrolyte that includes CaO as one of the constituents.
10 . The method defined in claim 1 wherein the electrolyte is a CaCl 2 -based electrolyte that includes CaO as one of the constituents and step (a) includes maintaining the cell potential above the decomposition potential for CaO.
11 . The method defined in claim 1 wherein the electrolyte is a CaCl 2 -based electrolyte that includes CaO as one of the constituents and step (a) includes maintaining the cell potential below the decomposition potential for CaCl 2 .
12 . The method defined in claim 1 wherein step (a) is carried out on a batch, continuous, or semi-continuous basis.
13 . The method defined in claim 1 wherein the processing in step (b) includes quenching from an elevated temperature to a lower temperature at which there is a comparatively low rate of oxidation of titanium metal in air.
14 . The method defined in claim 13 wherein the lower temperature is ambient temperature.
15 . The method defined in claim 13 wherein the quenching is conducted with water.
16 . The method defined in claim 2 wherein the forming includes compacting the titanium metal powder or pellet into a semi-finished or a ready-to-use product.
17 . The method defined in claim 16 wherein, in a situation in which the semi-finished or ready-to-use product is a sheet, step (b) includes the steps of roll compacting the titanium metal powders or pellet into a strip, sintering the strip to increase the mechanical properties of the strip, and cold rolling the sintered strip into a sheet.
18 . The method defined in claim 2 wherein step (b) includes processing the powder or pellet produced in step (a) by powder metallurgically processing the metal powder or pellet into a semi-finished or a ready-to-use product other than by roll compacting the powder or pellet.
19 . The method defined in claim 1 wherein the semi-finished or ready-to-use product includes products in sheet, bar, or tube forms.
20 . A titanium metal semi-finished or ready-to-use product having a concentration of chlorine of at least 100 ppm produced by the method defined in claim 1 .
21 . The titanium metal semi-finished or ready-to-use product defined in claim 20 wherein the chlorine concentration is at least 200 ppm.
22 . The titanium metal semi-finished or ready-to-use product defined in claim 20 wherein the chlorine concentration is at least 500 ppm.
23 . The titanium metal semi-finished or ready-to-use product defined in claim 20 wherein the chlorine concentration is at least 1000 ppm.
24 . The titanium metal semi-finished or ready-to-use product defined in claim 20 wherein the chlorine concentration is less than 2000 ppm.Cited by (0)
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